Analysis of trickle bed and packed bubble column bioreactors for combined carbon oxidation and nitrification



Título del documento: Analysis of trickle bed and packed bubble column bioreactors for combined carbon oxidation and nitrification
Revista: Brazilian journal of chemical engineering
Base de datos: PERIÓDICA
Número de sistema: 000308852
ISSN: 0104-6632
Autors: 1
2
3
Institucions: 1Laval University, Department of Chemical Engineering, Quebec. Canadá
2University Politehnica of Bucharest, Department of Chemical Engineering, Bucarest. Rumania
3University Politehnica of Bucharest, Department of Applied Physical Chemistry, Bucarest. Rumania
Any:
Període: Mar
Volum: 19
Número: 1
Paginació: 69-88
País: Brasil
Idioma: Inglés
Tipo de documento: Artículo
Enfoque: Experimental, aplicado
Resumen en inglés Biological removal of nitrogen and carbon by combined nitrification-oxidation in gas-liquid trickle-bed reactors (TBRs) and packed bubble columns (PBCs) was analyzed theoretically using a transient two-dimensional model. The model describes TBR and PBC performances at steady state as well as their transient response to a pulse or step increase in inlet methanol and NH4+-nitrogen concentrations. The hydrodynamic parameters were determined from residence time distribution measurements, using an imperfect pulse method for time-domain analysis of nonideal pulse tracer response. A transient diffusion model of the tracer in the porous particle coupled with the piston-dispersion-exchange model was used to interpret the residence time distribution curves obtained. Gas-liquid mass transfer parameters were determined by a stationary method based on the least-squares fit of the calculated concentration profiles in gas phase to the experimental values. Analysis of steady-state performances showed that under like operating conditions, the TBR outperforms the PBC in terms of conversions. A pulse change in the inlet methanol or NH4+-nitrogen concentration causes a negligible transient change in the outlet methanol concentration and a negligible or high transient change in the outlet NH4+-nitrogen concentration. A step change in the inlet methanol concentration causes the negligible transient change in the methanol outlet concentration and a relatively important transient change in the NH4+-nitrogen outlet concentration. A step increase in the NH4
Disciplines Química
Paraules clau: Ingeniería química,
Biotecnología,
Oxidación de carbono,
Nitrificación,
Reactores de lecho irrigado,
Columnas de lecho empacado
Keyword: Chemistry,
Chemical engineering,
Biotechnology,
Carbon oxidation,
Nitrification,
Trickle bed reactors,
Packed bed columns
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